• 한국물환경학회지
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• 제23권1호
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• pp.122-130
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• 2007

This study was conducted to evaluate water treatment characteristics according to vegetated wetland(V) and open water(O) arrangements in free water surface constructed wetland. Three pilot-scale wetlands, V-V, O-V and V-O, were built and operated. $BOD_5$ was a slightly reduced at all the arrangements because the influent concentration was so low as background concentration of constructed wetlands. While T-N and T-P removal efficiency showed higher than 50% for all cases. The O-V arrangement showed the highest removal efficiency: 20% for $BOD_5$, 56% for SS, 59% for T-N and 72% for T-P. Effluent concentration of the O-V were significantly low compared with those from the V-O. O-V arrangement would be beneficial in the light of pollutant removal efficiency as well as construction cost.

• KSBB Journal
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• 제14권5호
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• pp.606-610
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• 1999

본 연구는 회전생물활성탄 공정을 이용하여 부하를 증가시켜가면서 질소, 인 제거율을 조사하여 이들의 동시제거 가능성을 검토하였다. 암모니아성 질소 제거효율은 96.5% 이상으로 나타났으며 유출수의 암모니아성 질소, 아질산성 질소, 질산성 질소의 농도는 비교적 안정적으로 유지되었다. 총질소 제거율은 RUN 1을 제외하고는 90% 이상을 유지하였다. 총인은 32.7~49.8%의 제거율을 나타내었고 부하의 증가에 따라 부착미생물의 양은 269~473 mg/g support의 범위를 나타내었다.

• 대한환경공학회지
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• 제28권1호
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• pp.1-6
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• 2006

본 연구에서 수행한 입상형의 발포 폴리스티렌을 이용한 고도처리 공정은 기존의 상용화되거나 개발중인 영양염류 처리공정에 비해 수리학적 체류시간을 상당히 줄일 수 있고 동절기에도 온도의 영향을 크게 받지 않는 장점을 가지고 있다. 도시하수를 이용하여 bench-scale 연구를 수행한 결과 T-N 제거효율의 경우 HRT 6 hr 및 4 hr에서 각각 약 55% 및 51%로서 HRT가 짧아졌을때 단지 약 4%의 처리효율 감소가 관찰되었다. 온도 영향에 있어서 여름철과 겨울철의 T-N 제거효율을 비교해본 결과 T-N 제거 효율이 각각 약 65% 및 54%로 관찰되어 여름철이 겨울철에 비해 약 11% 더 높은 효율이 관찰되었으며 겨울철 효율저하는 주로 암모니아성 질소의 질산화가 원활이 이루어지지 않았기 때문인 것으로 관찰되었다. 유입부하 및 C/N 비에 관한 연구에서는 유량 및 농도의 변화가 심한 하 폐수 처리에 있어서도 안정된 처리수질을 확보할 수 있었으며, C/N 비가 감소에 따른 처리효율 저하가 크지 않음을 관찰 할 수 있었다. 따라서 본 개발 시스템을 기존의 중 소규모 하수처리장에 적용할 경우 유입수내의 유기물을 최대한 활용하여 영양염류를 처리할 수 있을 것이라 기대된다.

• 환경위생공학
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• 제13권1호
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• pp.91-103
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• 1998

Design data for COD and nitrogen removal from wastewater were collected from Pilot's Multi-stage Bio-reactor. Hyraulic conditions and pollutant loadings were varied in order to optimize the biological and operational parameters. Pilot's experimental results summarize as followings. 1. T-N removal efficiency in the organic volumetric loading 0.2 kgCOD/m$^{3}$·d was obtained as maxium of 85% at internal recycle ratio 2.5 and in more ratio than this it was decreased. Organic removal efficiency was about 91% under the overall experimental conditions and not influenced by recycle ratio.. 2. Nitrification reaction was shown as maxium in the SCOD$_{cr}$/NH$^{+}$-N ratio of 6.5 and in more ratio than this it was decreased. Denitrification rate was the maxium as 85% in more than 7.5 of SCOD$_{cr}$/NO$_{x}$-N ratio and in the ratio over this ratio it becomes constant. 3. By utilizing an applied new model of Stover-Kincannon from Monod's kinetic model, concentration of T-N in the effluent according to flow quanity in the influent was estimated as 8.74 and -67.5 respectively. The formula for estimating T-N concentration of effluent was obtained like this: N$_e$=N$_0$(1- $\frac{8.74}{(QN$_0$/A)-67.05}$)

• 한국지반환경공학회 논문집
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• 제8권6호
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• pp.21-28
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• 2007

본 연구는 합성하수 처리에 있어 MBR-RO 공정 적용시 유기물 및 질소, 인 제거에 대하여 수리학적체류시간이 제거효율에 미치는 영향을 실험적으로 검토하였다. MBR 공정에서 탁도는 운전기간(105일)동안 2 NTU 이하로 평균 99% 이상의 제거효율을 보였다 또한 수리학적체류시간 6, 12, 18 그리고 24 hour에 대한 $COD_{Cr}$, T-N, $NH_4{^+}-N$ 그리고 T-P의 평균 제거효율을 살펴보면, $COD_{Cr}$의 평균 제거율은 각각 72.4, 84, 88.6 그리고 92.5%, $NH_4{^+}-N$의 제거효율은 각각 60.2, 85.5, 91.3 그리고 92.2%였다. T-N과 T-P의 제거효율은 수리학적 체류시간을 6시간에서 24시간으로 증가시킴에 따라 각각 53.7과 56.8%에서 82.5와 86.4%로 증가했다. RO 공정에서 색도와 $COD_{Cr}$의 제거효율은 각각 99.9%와 96.8%였다. 또한 RO 유출수에서 T-N, $NH_4{^+}-N$, $NO_3{^-}-N$ 그리고 T-P는 평균 90% 이상 제거되었다.

• 한국환경보건학회지
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• 제26권3호
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• pp.92-97
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• 2000

The treatment of the washout from small scale incinerator was performed physically, chemically and biologically. The results are as follows. 1. SS, FS removal efficiency of washout wastewater from incinerator was 67.4%, 37.4%, while SS, FS of sewage wastewater was removed 63.2% 35.4% respectively. 2. The optimal conditions for chemical coagulation turned out to be pH 7.5, alum(Al2O3 10%) 30ml/ι and polyelectrolyte(A-601P 0.1%) 4ml/ι. SS 86%, FS 89.5%, BOD 42.5% and CODMn, 63.5% was removed and the removal efficiency of some metals are shown as Pb 93.5%, Zn 86.5% and Fe 80.6%. The concentration of the effluent was SS 9mg/ι, BOD 98.4mg/ι, and CODMn 138.4mg/ι. 3. The removal efficiency in treating washout wastewater of incinerator through HBC-briquet media was getting higher with increasing HRT, and mixed wastewater with 1:1, 1:2 ratio could be met up to the standard limit with higher HRT than 12hr. Under the condition of 1:2 mix ratio and HRT 24 hr, removal efficiency of SS, BOD, CODMn, T-N and T-P was 92.1%, 90%, 87%, 48.2% and 48%, respectively, and the concentration of treated wastewater was SS 2.9 mg/ι, BOD 10.3mg/ι, CODMn 14.1mg/ι, T-N 11.6 mg/ι and T-P 1.3 mg/ι, respectively.

• 한국환경보건학회지
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• 제23권1호
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• pp.43-49
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• 1997

This study was aimed to estimate removal efficiency(%) of BER(Biofilm-Electrode Reactor) and A.S(Activated Sludge) treatments. When were analyzed COD$_{Cr}$, NH$_3$-N and T-P by current density and reaction time, the results were as follows : 1) In BER treatment, the removal efficiency of COD$_{Cr}$ in domestic wastewater was 79-86% when current density was 2.39 mA/dm$2$(15mA)-3.98 mA/dm$^2$(25mA) and reaction time was 48 hr. 2) Removal efficiency of NH$_3$-N was 71-73% when current density was 2.39-3.98 mA/dm$^2$ and reaction time 48 hr. 3) When the reaction time was 48 hr removal efficiency(%) of BER treatment for COD$_{Cr}$, NH$_3$-N and T-P were more excellent than A.S. treatment. And then we prospect that was because activated microorganism colonies attached in biofilm on surface of electrode pannel. Therefore, In order to derive BER treatment efficiency(%) should establish optimum conditions of pH, temp., reaction time, current density and biochemical and electrochemical states.

• 한국물환경학회지
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• 제22권2호
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• pp.250-257
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• 2006

The objective of this study is to propose an alternative process for the small sewage treatment plants in rural communities. A biofilter has been used for biological wastewater treatment, which is becoming the alternative to the conventional activated sludge system. The proposed process used in this study, which is packed with floating media (i.e. expanded polystylene), has advantages of biofilter system and alternative flow system and they are incorporated into one process. Pilot and bench scale studies were performed using domestic wastewater. In the results of pilot plant study, it was observed that the stable effluent water quality was achieved and it met the present effluent criteria of suspended solid (SS), organic matters, T-N and T-P. In the study for determination of the cycle of backwashing, it was observed that the cycle of backwashing depended on BOD loading rates of influents. In the BOD loading rates of $0.5kg\;BOD/m^3{\cdot}day$ and $1.0kg\;BOD/m^3{\cdot}day$, the backwashing cycle of 28 hour and 16 hour were needed, respectively. The optimum backwashing time was 120~80 seconds at the media expansion rate of 50%. In the removal of SS, organic matters, T-N and T-P, SS removal was rather achieved by physical filtration than biological mechanism and the removal of organic matters except for SS, T-N and T-P were mainly rather achieved by biological mechanism than physical filtration. In bench-scale study, the effects of recirculation rate was investigated on removal of SS, TCOD, T-N and T-P. It was observed that the recirculation made removal efficiencies of SS, TCOD, T-N and T-P increased. Especially, in T-N removal, the increase of T-N removal efficiency of 40% was observed in the reicirculation rate of 1Q compared with 0Q.

• 한국물환경학회지
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• 제22권2호
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• pp.203-208
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• 2006

A continuous feed and cyclic draw SBR process was developed to overcome flow rate fluctuation and to maximize organic matters utilization efficiency for nitrogen and phosphorus removal. The developed SBR process was operated with two parallel reactors. Influent was supplied to one reactor which was not obligately aerated. At the same time, the other reactor was just aerated without supplying influent. In addition this mode was changed periodically. Cycle time was 6hr and aeration time ratio($t_{aer}/t_{total}$) was 0.33, respectively. $COD_{cr}$ and SS removal efficiencies of 95% or higher were achieved. Nitrogen removal was so greatly influenced by influent $COD_{cr}/T-N$ ratio. At influent $COD_{cr}/T-N$ ratio of 5.7, removal efficiencies of ammonia-N, T-N and T-P were 96%, 78% and 55%, respectively. Influent $COD_{cr}/T-N$ of 4 or higher ratio was necessary to achieve 60% or higher nitrogen removal. Organic matters of influent was efficiently utilized in denitrification reaction and consumed COD has a good correlation with removed T-N(about 6.5 mgCOD/mgTN). Continuous feed and cyclic draw SBR process could be one of alternative processes for the removal of nutrients in rural area where $COD_{cr}/T-N$ ratio was low and fluctuation of flow rate was severe.

• 한국환경농학회지
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• 제19권2호
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• pp.134-141
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• 2000

전기화학적 방법을 이용한 농공단지폐수의 효율적인 처리기술개발을 위한 기초실험으로서 전압, 전극판 간격, pH 및 전해용액 주입농도 등에 따른 오염물질 처리효율을 조사한 결과는 다음과 같다. 전압별 전기화학반응조내 온도 및 pH는 전압이 높을수록 상승하였으나, EC는 전압별로 별 변화가 없었다. COD, 탁도, T-N 및 T-P의 처리율은 전압이 높을수록 증가하였으며 전압 20V일 경우 COD는 20분, 탁도는 30분, T-N 및 T-P는 2분일 때 각각 그 처리율이 약 65, 90, 68 및 84%로 가장 높았다. 전극판 간격별 COD 처리율은 전극간격이 좁아질수록 그리고 전기반응시간이 경과할수록 전반적으로 증가하는 경향이었으며, 탁도 처리율은 전극판 간격 모두 전기반응초기에 약 80%이상 처리되었고, T-N 처리율은 전극판 간격이 좁을수록 높았다. T-P 처리율은 전기반응시간 2분 후에 전극판 간격 모두에서 약 79% 이상 처리되었다. 초기 pH에 따른 COD 처리율은 전반적으로 pH 7에서 높았으며, 탁도 처리율은 전기반응시간 2분 이후의 모든 조건에서 약 80%이상 처리되었다. 그리고 T-N 처리율은 초기 pH가 높아질수록 증가하였고, T-P 처리율은 전기반응시간 2분 이후 초기 $pH\;5{\sim}9$에서 약 $79{\sim}96%$로서 가장 높았다. NaCl 농도별 오염물질 처리율은 전반적으로 NaCl을 주입한 경우가 NaCl를 주입하지 않은 경우에 비해 매우 높았으며, COD 및 T-P의 처리율은 $NaCl\;500mg/l$, 탁도 처리율은 $NaCl\;1,000mg/l$, T-N의 처리율은 NaCl 250 및 $500mg/l$에서 전반적으로 다른 조건에 비하여 높았다.